METHODS AND SYSTEMS EMPLOYING A HORIZONTALLY CONFIGURED DIGESTION UNIT FOR HYDROTHERMAL DIGESTION OF CELLULOSIC BIOMASS SOLIDS
    382.
    发明申请
    METHODS AND SYSTEMS EMPLOYING A HORIZONTALLY CONFIGURED DIGESTION UNIT FOR HYDROTHERMAL DIGESTION OF CELLULOSIC BIOMASS SOLIDS 有权
    使用水平生物质固体水热消解的水平配置消毒装置的方法和系统

    公开(公告)号:US20140330049A1

    公开(公告)日:2014-11-06

    申请号:US14264724

    申请日:2014-04-29

    Abstract: Biomass compaction during hydrothermal digestion of cellulosic biomass solids may become problematic, particularly as the vertical height of a cellulosic biomass charge increases. Compaction may be decreased in a horizontally configured hydrothermal digestion unit. Methods for digesting cellulosic biomass solids may comprise: providing a hydrothermal digestion unit having a length or a width greater than its height and containing a fluid phase digestion medium and a slurry catalyst capable of activating molecular hydrogen; introducing cellulosic biomass solids to the hydrothermal digestion unit; distributing the cellulosic biomass solids laterally within the hydrothermal digestion unit; after or while the cellulosic biomass solids are being distributed, supplying an upwardly directed flow of molecular hydrogen through the cellulosic biomass solids and the fluid phase digestion medium; and heating the cellulosic biomass solids in the presence of the slurry catalyst and the molecular hydrogen, thereby forming an alcoholic component derived from the cellulosic biomass solids.

    Abstract translation: 在纤维素生物质固体的热液消解过程中的生物量压实可能变得有问题,特别是随着纤维素生物质电荷的垂直高度增加。 在水平配置的水热消解装置中压实可能会减少。 消化纤维素生物质固体的方法可以包括:提供具有大于其高度的长度或宽度的水热消化单元,并且含有流体相消化介质和能够活化分子氢的淤浆催化剂; 将纤维素生物质固体引入水热消解单元; 在水热消解单元内横向分布纤维素生物质固体; 在分配纤维素生物质固体之后或同时,通过纤维素生物质固体和流体相消化介质供应向上指向的分子氢流; 并在浆料催化剂和分子氢的存在下加热纤维素生物质固体,从而形成衍生自纤维素生物质固体的醇组分。

    PROCESS FOR CONVERTING A BIOMASS MATERIAL
    383.
    发明申请
    PROCESS FOR CONVERTING A BIOMASS MATERIAL 审中-公开
    转化生物质材料的方法

    公开(公告)号:US20140325896A1

    公开(公告)日:2014-11-06

    申请号:US14265428

    申请日:2014-04-30

    Abstract: A process for converting a biomass material comprising a) pyrolyzing a biomass material to produce a biomass-derived pyrolysis product; b) providing a petroleum-derived hydrocarbon composition having a C7-asphaltenes content of equal to or more than 0.2 wt %, based on the total weight of the petroleum-derived hydrocarbon composition, which petroleum-derived hydrocarbon composition has a total acid number of equal to or more than 0.5 mg KOH/g and/or a density at 15.5° C. of equal to or more than 0.8 grams/ml and/or a viscosity at 37.8° C. of equal to or more than 500 centiStokes (cSt); c) mixing at least part of the biomass-derived pyrolysis product and at least part of the petroleum-derived hydrocarbon composition to produce a hydrocarbon-containing mixture; and d) dewatering the hydrocarbon-containing mixture to produce a dewatered hydrocarbon-containing mixture.

    Abstract translation: 一种用于转化生物质材料的方法,包括a)热解生物质材料以产生生物质衍生的热解产物; b)基于石油衍生的烃组合物的总重量,提供具有等于或大于0.2重量%的C7-沥青质含量的石油衍生的烃组合物,该石油衍生烃组合物的总酸值为 等于或大于0.5mg KOH / g和/或15.5℃下的密度等于或大于0.8克/毫升和/或在37.8℃下的粘度等于或大于500厘沲(cSt ); c)将至少部分生物质衍生的热解产物和至少部分来自石油的烃组合物混合以产生含烃混合物; 和d)使含烃混合物脱水以产生脱水的含烃混合物。

    PRODUCTION OF SYNTHESIS GAS
    385.
    发明申请
    PRODUCTION OF SYNTHESIS GAS 审中-公开
    合成气的生产

    公开(公告)号:US20140311884A1

    公开(公告)日:2014-10-23

    申请号:US14352070

    申请日:2012-10-17

    CPC classification number: C10B21/00 C01B3/363 F23D14/22 F23D17/002

    Abstract: Process and reactor for the production of synthesis gas by partial combustion of a hydrocarbon feed. A burner is used with a plurality of coaxial burner channels, wherein at least one channel supplies a flow of a non-gaseous hydrocarbon feed, at least one other channel supplies a flow containing a gaseous hydrocarbon feed and at least one further channel supplies a non-hydrocarbon moderator gas.

    Abstract translation: 用于通过烃进料的部分燃烧生产合成气的方法和反应器。 燃烧器与多个同轴燃烧器通道一起使用,其中至少一个通道供应非气态烃进料的流,至少一个其它通道提供含有气态烃进料的流,并且至少一个另外的通道提供非气态烃进料, - 烃缓和剂气体。

    Olefin epoxidation process
    387.
    发明授权
    Olefin epoxidation process 有权
    烯烃环氧化工艺

    公开(公告)号:US08859792B2

    公开(公告)日:2014-10-14

    申请号:US13950359

    申请日:2013-07-25

    CPC classification number: C07D301/10 C07D301/04

    Abstract: A process for the production of an olefin oxide, which process comprises reacting a feed comprising an olefin and oxygen in a reactor tube in the presence of a silver-containing catalyst, wherein the presence of water in the catalyst bed is controlled such that the ratio of the partial pressure of water (PPH2O) divided by the vapor pressure of water (VPH2O) is less than 0.006, preferably less than 0.004.

    Abstract translation: 一种生产烯烃氧化物的方法,该方法包括在含银催化剂存在下,使反应器管中含有烯烃和氧的进料反应,其中催化剂床中的水的存在被控制, 的水分压(PPH2O)除以水的蒸气压(VPH2O)小于0.006,优选小于0.004。

    PROCESS FOR THE FLUID CATALYTIC CRACKING OF OXYGENATED HYDROCARBON COMPOUNDS FROM BIOLOGICAL ORIGIN
    388.
    发明申请
    PROCESS FOR THE FLUID CATALYTIC CRACKING OF OXYGENATED HYDROCARBON COMPOUNDS FROM BIOLOGICAL ORIGIN 审中-公开
    来自生物原料的含氧化合物的流体催化裂化工艺

    公开(公告)号:US20140296592A1

    公开(公告)日:2014-10-02

    申请号:US14227621

    申请日:2014-03-27

    Abstract: A process for the fluid catalytic cracking of oxygenated hydrocarbon compounds from biological origin. The process comprises (a) contacting a feed comprising the oxygenated hydrocarbon compounds with a fluid catalytic cracking catalyst at elevated temperature to produce a cracked products stream, the feed comprising an amount of sulphur; (b) separating catalyst from the cracked products stream; (c) separating a light fraction from the cracked products stream; and (d) removing hydrogen sulphide from the light fraction by means of an amine treating process. The fluid catalytic cracking process involves the presence or use of water and/or steam and comprises a working-up process of the cracked products stream. In the working-up process, one or more chemical additives for reducing or hindering the formation of foam in amine liquids selected from defoamers and demulsifiers are added to the amine solvent in one or more amine treaters.

    Abstract translation: 一种从生物来源对含氧化合物进行流化催化裂化的方法。 该方法包括(a)在升高的温度下将包含含氧烃化合物的进料与流化催化裂化催化剂接触以产生裂化产物流,所述进料包含一定量的硫; (b)从裂化产物流中分离催化剂; (c)从裂化产物流中分离轻馏分; 和(d)通过胺处理方法从轻馏分中除去硫化氢。 流化催化裂化过程涉及水和/或蒸汽的存在或使用,并且包括裂化产物流的处理过程。 在后处理过程中,将一种或多种用于减少或阻碍选自消泡剂和破乳剂的胺液体中的泡沫形成的化学添加剂加入到一种或多种胺处理剂中的胺溶剂中。

    METHODS FOR DIGESTION OF CELLULOSIC BIOMASS SOLIDS IN THE PRESENCE OF A PHENOLIC SOLVENT GENERATED IN SITU FROM LIGNIN
    389.
    发明申请
    METHODS FOR DIGESTION OF CELLULOSIC BIOMASS SOLIDS IN THE PRESENCE OF A PHENOLIC SOLVENT GENERATED IN SITU FROM LIGNIN 有权
    在由Lignin生成的酚醛溶剂存在下消除细胞生物质固体的方法

    公开(公告)号:US20140275513A1

    公开(公告)日:2014-09-18

    申请号:US14207786

    申请日:2014-03-13

    Abstract: Digestion of cellulosic biomass solids can be enhanced in the presence of a phenolic solvent. Methods for digesting cellulosic biomass solids can comprise providing cellulosic biomass solids in a digestion medium comprising water and an organic solvent; heating the cellulosic biomass solids and the digestion medium in a digestion unit in the presence of molecular hydrogen and a slurry catalyst capable of activating molecular hydrogen, thereby forming an alcoholic component and liberating lignin, the lignin forming a phenolics liquid phase partitioned from the digestion medium and at least a portion of the slurry catalyst accumulating in the phenolics liquid phase; removing at least a portion of the phenolics liquid phase and accumulated slurry catalyst from the digestion unit; converting at least a portion of the phenolics liquid phase into a phenolic solvent; and returning at least a portion of the phenolic solvent and the slurry catalyst to the digestion unit.

    Abstract translation: 可以在酚类溶剂的存在下提高纤维素生物质固体的消化。 消化纤维素生物质固体的方法可以包括在包含水和有机溶剂的消化介质中提供纤维素生物质固体; 在分子氢和能够活化分子氢的浆料催化剂存在下,在消化单元中加热纤维素生物质固体和消化介质,由此形成醇组分和释放木质素,木质素形成从消化介质分配的酚类液相 并且至少一部分浆料催化剂积聚在酚醛液相中; 从消化单元中除去至少一部分酚类液相和累积的浆料催化剂; 将至少一部分酚类液相转化成酚类溶剂; 并将至少一部分酚类溶剂和浆料催化剂返回到消化单元。

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